CA2700098C - Bubble column type hydrocarbon synthesis reactor, and hydrocarbon synthesis reaction system having the same - Google Patents

Bubble column type hydrocarbon synthesis reactor, and hydrocarbon synthesis reaction system having the same Download PDF

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Publication number
CA2700098C
CA2700098C CA2700098A CA2700098A CA2700098C CA 2700098 C CA2700098 C CA 2700098C CA 2700098 A CA2700098 A CA 2700098A CA 2700098 A CA2700098 A CA 2700098A CA 2700098 C CA2700098 C CA 2700098C
Authority
CA
Canada
Prior art keywords
main body
reactor
cooling fluid
introducing
slurry
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CA2700098A
Other languages
English (en)
French (fr)
Other versions
CA2700098A1 (en
Inventor
Yasuhiro Onishi
Yuzuru Kato
Eiichi Yamada
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Cosmo Oil Co Ltd
Japan Petroleum Exploration Co Ltd
Inpex Corp
Japan Oil Gas and Metals National Corp
Nippon Steel Engineering Co Ltd
Eneos Corp
Original Assignee
Cosmo Oil Co Ltd
Japan Petroleum Exploration Co Ltd
Inpex Corp
Japan Oil Gas and Metals National Corp
Nippon Oil Corp
Nippon Steel Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Cosmo Oil Co Ltd, Japan Petroleum Exploration Co Ltd, Inpex Corp, Japan Oil Gas and Metals National Corp, Nippon Oil Corp, Nippon Steel Engineering Co Ltd filed Critical Cosmo Oil Co Ltd
Publication of CA2700098A1 publication Critical patent/CA2700098A1/en
Application granted granted Critical
Publication of CA2700098C publication Critical patent/CA2700098C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34—Apparatus, reactors
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • C10G2/344—Apparatus, reactors with moving solid catalysts according to the "fluidised-bed" technique
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00141—Coils
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • B01J2208/00336—Controlling the temperature by direct heat exchange adding a temperature modifying medium to the reactants
    • B01J2208/00353—Non-cryogenic fluids
    • B01J2208/00362—Liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • B01J2208/00336—Controlling the temperature by direct heat exchange adding a temperature modifying medium to the reactants
    • B01J2208/00353—Non-cryogenic fluids
    • B01J2208/00371—Non-cryogenic fluids gaseous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00259—Preventing runaway of the chemical reaction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00272—Addition of reaction inhibitor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
CA2700098A 2007-09-27 2008-09-26 Bubble column type hydrocarbon synthesis reactor, and hydrocarbon synthesis reaction system having the same Expired - Fee Related CA2700098C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2007-252521 2007-09-27
JP2007252521 2007-09-27
PCT/JP2008/067469 WO2009041604A1 (ja) 2007-09-27 2008-09-26 気泡塔型炭化水素合成反応器及びこれを備える炭化水素合成反応システム

Publications (2)

Publication Number Publication Date
CA2700098A1 CA2700098A1 (en) 2009-04-02
CA2700098C true CA2700098C (en) 2013-04-30

Family

ID=40511484

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2700098A Expired - Fee Related CA2700098C (en) 2007-09-27 2008-09-26 Bubble column type hydrocarbon synthesis reactor, and hydrocarbon synthesis reaction system having the same

Country Status (11)

Country Link
US (1) US20100247392A1 (ru)
EP (1) EP2199368B8 (ru)
JP (1) JP5220755B2 (ru)
CN (1) CN101918514A (ru)
AU (1) AU2008304826B8 (ru)
BR (1) BRPI0817733A2 (ru)
CA (1) CA2700098C (ru)
EA (1) EA017888B1 (ru)
MY (1) MY152110A (ru)
WO (1) WO2009041604A1 (ru)
ZA (1) ZA201002078B (ru)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5802397B2 (ja) * 2011-01-31 2015-10-28 独立行政法人石油天然ガス・金属鉱物資源機構 温度制御システム
JP5950500B2 (ja) * 2011-03-17 2016-07-13 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素の製造装置及び炭化水素の製造方法
JP5808559B2 (ja) 2011-03-31 2015-11-10 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素油の製造方法、フィッシャー・トロプシュ合成反応装置及び炭化水素油の製造システム
JP5815324B2 (ja) * 2011-08-05 2015-11-17 独立行政法人石油天然ガス・金属鉱物資源機構 温度制御システム
US8889747B2 (en) * 2011-10-11 2014-11-18 Bp Corporation North America Inc. Fischer Tropsch reactor with integrated organic rankine cycle
CN103285784B (zh) * 2013-06-13 2016-03-23 神华集团有限责任公司 费托合成三相浆态床及其反应器
JP6518108B2 (ja) * 2015-03-30 2019-05-22 株式会社クボタ 気泡塔型スラリー床反応装置
JP6518480B2 (ja) * 2015-03-30 2019-05-22 株式会社クボタ 気泡塔型スラリー床反応装置
CN113563923A (zh) * 2021-08-19 2021-10-29 中国石油化工股份有限公司 一种汽油加氢方法及汽油加氢装置

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2161974A (en) * 1937-01-21 1939-06-13 Standard Oil Dev Co Method of controlling exothermic reactions
US5900159A (en) * 1996-02-29 1999-05-04 Shell Oil Company Method for separating liquid from a slurry
US6160026A (en) * 1997-09-24 2000-12-12 Texaco Inc. Process for optimizing hydrocarbon synthesis
WO2002031083A2 (en) * 2000-10-13 2002-04-18 Bp Exploration Operating Company Limited Fischer-tropsch synthesis process
GB2382786B (en) * 2001-12-04 2005-10-19 Sasol Technology Slurry phase apparatus
US6822006B1 (en) * 2003-07-02 2004-11-23 Chevron U.S.A. Inc. Methods of controlling the temperature of an exothermic reaction
JP2007252521A (ja) 2006-03-22 2007-10-04 Daiichi Shokai Co Ltd 遊技機

Also Published As

Publication number Publication date
EP2199368A1 (en) 2010-06-23
EA017888B1 (ru) 2013-03-29
ZA201002078B (en) 2011-05-25
JP5220755B2 (ja) 2013-06-26
US20100247392A1 (en) 2010-09-30
MY152110A (en) 2014-08-15
WO2009041604A1 (ja) 2009-04-02
AU2008304826A1 (en) 2009-04-02
EP2199368B1 (en) 2013-06-05
AU2008304826B8 (en) 2011-10-27
CA2700098A1 (en) 2009-04-02
JPWO2009041604A1 (ja) 2011-01-27
BRPI0817733A2 (pt) 2015-03-31
EP2199368A4 (en) 2011-12-14
EP2199368B8 (en) 2013-09-11
AU2008304826B2 (en) 2011-09-08
EA201070311A1 (ru) 2010-10-29
CN101918514A (zh) 2010-12-15

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Effective date: 20150928